JPH04500626A - osmotic absorbent - Google Patents
osmotic absorbentInfo
- Publication number
- JPH04500626A JPH04500626A JP1510167A JP51016789A JPH04500626A JP H04500626 A JPH04500626 A JP H04500626A JP 1510167 A JP1510167 A JP 1510167A JP 51016789 A JP51016789 A JP 51016789A JP H04500626 A JPH04500626 A JP H04500626A
- Authority
- JP
- Japan
- Prior art keywords
- osmotic
- promoter
- absorber
- polymer
- osmotic pressure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 230000003204 osmotic effect Effects 0.000 title description 52
- 239000002250 absorbent Substances 0.000 title description 21
- 230000002745 absorbent Effects 0.000 title description 21
- 239000006096 absorbing agent Substances 0.000 description 30
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 26
- 239000012528 membrane Substances 0.000 description 25
- 239000007788 liquid Substances 0.000 description 24
- 229920000642 polymer Polymers 0.000 description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 16
- 238000010521 absorption reaction Methods 0.000 description 13
- 239000011780 sodium chloride Substances 0.000 description 13
- 229920002301 cellulose acetate Polymers 0.000 description 9
- 239000000835 fiber Substances 0.000 description 9
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 6
- 239000008103 glucose Substances 0.000 description 6
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 239000002023 wood Substances 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 229920001778 nylon Polymers 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 239000004677 Nylon Substances 0.000 description 4
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 4
- 239000012510 hollow fiber Substances 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 3
- 229930006000 Sucrose Natural products 0.000 description 3
- 238000000502 dialysis Methods 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 229920005597 polymer membrane Polymers 0.000 description 3
- 229910052700 potassium Inorganic materials 0.000 description 3
- 239000011591 potassium Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 230000035882 stress Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000005720 sucrose Substances 0.000 description 3
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- -1 For example Polymers 0.000 description 2
- 229910013470 LiC1 Inorganic materials 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 2
- 229920002522 Wood fibre Polymers 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000004132 cross linking Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000002427 irreversible effect Effects 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 229920002492 poly(sulfone) Polymers 0.000 description 2
- 229920000570 polyether Polymers 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- FGDZQCVHDSGLHJ-UHFFFAOYSA-M rubidium chloride Chemical compound [Cl-].[Rb+] FGDZQCVHDSGLHJ-UHFFFAOYSA-M 0.000 description 2
- 235000017557 sodium bicarbonate Nutrition 0.000 description 2
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 241000894007 species Species 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- 239000002025 wood fiber Substances 0.000 description 2
- GHPYJLCQYMAXGG-WCCKRBBISA-N (2R)-2-amino-3-(2-boronoethylsulfanyl)propanoic acid hydrochloride Chemical compound Cl.N[C@@H](CSCCB(O)O)C(O)=O GHPYJLCQYMAXGG-WCCKRBBISA-N 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- 241000283690 Bos taurus Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 239000001856 Ethyl cellulose Substances 0.000 description 1
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 229920001007 Nylon 4 Polymers 0.000 description 1
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 108091006629 SLC13A2 Proteins 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 150000003868 ammonium compounds Chemical class 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- WDIHJSXYQDMJHN-UHFFFAOYSA-L barium chloride Chemical compound [Cl-].[Cl-].[Ba+2] WDIHJSXYQDMJHN-UHFFFAOYSA-L 0.000 description 1
- 229910001626 barium chloride Inorganic materials 0.000 description 1
- UWCPYKQBIPYOLX-UHFFFAOYSA-N benzene-1,3,5-tricarbonyl chloride Chemical compound ClC(=O)C1=CC(C(Cl)=O)=CC(C(Cl)=O)=C1 UWCPYKQBIPYOLX-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 125000005442 diisocyanate group Chemical group 0.000 description 1
- 229920001249 ethyl cellulose Polymers 0.000 description 1
- 235000019325 ethyl cellulose Nutrition 0.000 description 1
- 230000006355 external stress Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000003349 gelling agent Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000001631 haemodialysis Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000000322 hemodialysis Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000004941 influx Effects 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 229920000831 ionic polymer Polymers 0.000 description 1
- 239000012948 isocyanate Substances 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- VQTGUFBGYOIUFS-UHFFFAOYSA-N nitrosylsulfuric acid Chemical compound OS(=O)(=O)ON=O VQTGUFBGYOIUFS-UHFFFAOYSA-N 0.000 description 1
- GSWAOPJLTADLTN-UHFFFAOYSA-N oxidanimine Chemical compound [O-][NH3+] GSWAOPJLTADLTN-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229920001467 poly(styrenesulfonates) Polymers 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229960002796 polystyrene sulfonate Drugs 0.000 description 1
- 239000011970 polystyrene sulfonate Substances 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 229910052701 rubidium Inorganic materials 0.000 description 1
- IGLNJRXAVVLDKE-UHFFFAOYSA-N rubidium atom Chemical compound [Rb] IGLNJRXAVVLDKE-UHFFFAOYSA-N 0.000 description 1
- 229940102127 rubidium chloride Drugs 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000011550 stock solution Substances 0.000 description 1
- 125000000185 sucrose group Chemical group 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- ILJSQTXMGCGYMG-UHFFFAOYSA-N triacetic acid Chemical compound CC(=O)CC(=O)CC(O)=O ILJSQTXMGCGYMG-UHFFFAOYSA-N 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/16—Drying solid materials or objects by processes not involving the application of heat by contact with sorbent bodies, e.g. absorbent mould; by admixture with sorbent materials
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L15/00—Chemical aspects of, or use of materials for, bandages, dressings or absorbent pads
- A61L15/16—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons
- A61L15/18—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons containing inorganic materials
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L15/00—Chemical aspects of, or use of materials for, bandages, dressings or absorbent pads
- A61L15/16—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons
- A61L15/22—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons containing macromolecular materials
- A61L15/28—Polysaccharides or their derivatives
Landscapes
- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Epidemiology (AREA)
- Materials Engineering (AREA)
- Animal Behavior & Ethology (AREA)
- Hematology (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Inorganic Chemistry (AREA)
- Molecular Biology (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- External Artificial Organs (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 浸透圧吸収剤 発明の背景 大ていの天然繊維と合成繊維は限定された液体貯蔵能を有する;しかじ、繊維が 通常のやり方で液体を貯蔵するならば、繊維は何らかの応力を受けたときにこの 液体を放出することができない、このような物質は液体の吸収が必要である場合 に、広範囲な用途を見出している0例えば、吸収性を有する繊維は使い捨て吸収 体製品に用いられる。これらの製品にはおむつ、女性用衛生製品、病院用使い捨 て製品(hospital disposable)、外科用包帯、および工業 用ワイプ(industr−ial wipe)があり、これらの使い捨て吸収 体製品の最大の市場はベビー用おむつである。現在、使い捨ておむつは吸収体と してウッドフラフ(wood fluff)か超吸収体(superabsor ben t)ポリマーゲルウフドフラフとの組合せのいずれかを用いている。[Detailed description of the invention] osmotic absorbent Background of the invention Most natural and synthetic fibers have limited liquid storage capacity; If a liquid is stored in the normal way, the fibers will react to this when subjected to some stress. If such substances are unable to release liquid and require liquid absorption For example, absorbent fibers have found a wide range of uses in disposable absorbent Used in body products. These products include diapers, feminine hygiene products, and hospital disposables. products (hospital disposable), surgical bandages, and industrial There are industrial-ial wipes, and these disposable absorbent The largest market for body products is baby diapers. Currently, disposable diapers are made of absorbent materials. Wood fluff or superabsor Bent) using any of the following combinations with polymer gel powder fluff.
ウソドフラフは、個々の繊維が通常は長く、薄いリボンとして、約20〜約10 0ミクロンの範囲内の断面サイズを有する木材繊維のブレンドから成る0個々の 繊維の密度は約0. 9〜約1.1g/cjの範囲内である。しかし、おむつに 吸収体マットとして用いられる場合のウッドフラフは0.0Rg /cjの好ま しいかぎ密度を有する。この密度差が個々の繊維の間に大きい空隙容積を形成し 、ここに吸収された液体が貯蔵される。しかし、この液体は毛管作用力によって 繊維の外面に維持されるので、この液体は応力によって容易に放出される。ウッ ドフラフの容量が1.0OOGの応力下では約xog/gから約1 g/gまで に低下することが報告されている。それ故、吸収体としてウッドフラフを用いた おむつは液体含量を低下させ、非常に種々な問題を生ずる。Usodofuraf has individual fibers that are usually long, thin ribbons of about 20 to about 10 0 individual consisting of a blend of wood fibers with a cross-sectional size in the range of 0 microns The fiber density is approximately 0. It is within the range of 9 to about 1.1 g/cj. But in diapers Wood fluff when used as an absorbent mat has a preferable value of 0.0Rg/cj. It has a high key density. This density difference creates a large void volume between individual fibers. , where the absorbed liquid is stored. However, due to capillary action, this liquid Since it is maintained on the outer surface of the fibers, this liquid is easily released by stress. Ugh Under a stress of 1.0OOG, the capacitance of Dofurafu ranges from about xog/g to about 1 g/g. It has been reported that there is a decrease in Therefore, wood fluff was used as an absorbent material. Diapers reduce fluid content, creating a wide variety of problems.
本発明の請求項に述べる浸透圧吸収体(os+wotic absorbent )は膜シェル(we■−brans 5hell)内に水を封入する膨張膜系で ある。この容積膨張はより大きな吸収容量が得られる機構であるので、本発明の 重要な一面である0例えばウッドフラフのような静止非膨張性構造体に比べて、 浸透圧による容積膨張はこれらの浸透圧吸収体によって観察される2100重量 %以上までの吸収空間(space for uptake)を形成する。Osmotic pressure absorber (os+wotic absorbent) stated in the claims of the present invention ) is an expanding membrane system that seals water inside the membrane shell (we■-brans 5hell). be. This volume expansion is the mechanism by which a larger absorption capacity can be obtained, so the present invention One important aspect is that compared to static, non-expandable structures such as wood fluff, The osmotic volume expansion observed by these osmotic absorbers is 2100 wt. % or more of absorption space.
おむつ用途に用いられる趙吸収体ポリマー(AGM’ s)は少ない割合の架橋 を含む高分子量イオンポリマーである。AGM’ sにおけるこの架橋密度の制 御は水に不溶な粒子と、容積膨張のための膨潤容量とを生ずる。米国特許第4, 703.067号は外部加熱なしの重合による固体の吸水性架橋ポリアクリレー ト樹脂の製造方法を述べている。米国特許第4,677.174号は種々なモノ マーの水性重合によって製造された吸水性架橋アクリレート樹脂コポリマーを述 べている。いずれの場合にも、これらの浸透圧吸収体によるような膜構造体は含 まれていない0本発明の浸透圧吸収体は容積膨張系である点でAGM’ sの有 利な面を含む、。Zhao absorbent polymers (AGM’s) used in diaper applications have a small proportion of crosslinking. is a high molecular weight ionic polymer containing Control of this crosslinking density in AGM’s The control produces particles that are insoluble in water and a swelling capacity for volume expansion. U.S. Patent No. 4, No. 703.067 is a solid water-absorbing crosslinked polyacrylate produced by polymerization without external heating. This paper describes a method for producing the resin. U.S. Patent No. 4,677.174 covers various describes a water-absorbing cross-linked acrylate resin copolymer produced by aqueous polymerization of I'm looking forward to it. In either case, membrane structures such as these osmotic absorbers are not included. The osmotic pressure absorber of the present invention has the advantage of AGM's in that it is a volume expansion system. Including advantageous aspects.
AGM’ sはおむつ心部内のウッドフラフマトリックスによって支持される顆 粒として典型的に分散される。木材繊維の薄いリボン状の性質がおむつ心部内へ の液体の捕捉と分布とに役立ち、AGMは不可逆的な貯蔵のためのビヒクルとし て役立つ、それ故、本発明の浸透圧吸収体の他の利点は改良された不可逆的液体 貯蔵である。AGM’s condyle is supported by a Woodfluff matrix within the diaper core. Typically dispersed as granules. The thin ribbon-like nature of wood fibers enters the core of the diaper. AGM serves as a vehicle for irreversible storage, helping to capture and distribute liquids. Therefore, another advantage of the osmotic absorber of the present invention is improved irreversible liquid It is storage.
これらの浸透圧吸収体は膜成分を含む、これは拡散制御プロセスでシェル中に液 体を吸収し、分子は浸透圧勾配経路(oawotic gradient pa thwaいを横切って拡散する。外部応力と外力は必要なく、導入されないので 、流量は通常の逆浸這(RO)膜作用の場合に達成される流量よりも寓質的に低 い、ある点では、すなわち適用圧力の低下が小さいかまたは全て存在しない場合 には、本発明の浸透圧吸収体は透析プロセスを含む、13折は、液体状態での重 要な差異がそれらの溶賀の化学的ポテンシャルである場合に主要な効果が一つの 液体から他の液体への0賀分子の転移であるプロセスとして定義されている0例 えば血液透析に用いられるような通常の透析膜は1000原子質置単位以上の分 子量カットオフ(molecularweight cutoff)を有する。These osmotic absorbers contain a membrane component, which allows liquid to flow into the shell in a diffusion-controlled process. The body absorbs the molecules, which pass through the osmotic gradient pathway (oawotic gradient path). spread across the thwa. Since external stresses and forces are not required and are not introduced , the flow rate is allegorically lower than that achieved in the case of normal reverse osmosis (RO) membrane action. Yes, in some respects, i.e. when the applied pressure drop is small or not present at all. The osmotic absorber of the present invention involves a dialysis process. The main effect is one when the key difference is the chemical potential of their melts. 0 example defined as a process that is the transfer of 0 molecules from one liquid to another For example, a normal dialysis membrane used for hemodialysis has a molecular weight of more than 1000 atomic units. It has a molecular weight cutoff.
浸透圧は数依存性現象であり;それ故、浸透圧差からの高い流量は単位面積あた り多数の分子を必要とする。従って、これらの浸透圧吸収体のプロモーター成分 は重量と容積(volume)効果の両方に対して500原子質量単位未満の低 分子量種である。透析とは正反対に、これらの浸透圧吸収剤はROまたは超濾過 性を有する膜成分を用いる。Osmotic pressure is a number-dependent phenomenon; therefore, high flow rates from osmotic pressure differences are requires a large number of molecules. Therefore, the promoter components of these osmotic absorbers has a low value of less than 500 atomic mass units for both weight and volume effects. It is a molecular weight species. In direct contrast to dialysis, these osmotic absorbers can be used for RO or ultrafiltration. Use membrane components that have properties.
以下でさらに詳述するように、液体でのその重量の数倍を吸収し、吸収液体量が 前記先行技術吸収体に吸収される液体量より多い浸透圧吸収体が製造されること が今回発見された。absorbs several times its weight in liquid, and the amount of liquid absorbed increases, as detailed further below. The osmotic absorber is manufactured in an amount greater than the amount of liquid absorbed by said prior art absorber. was discovered this time.
発−所−9−概一要 既述したように、使い捨て吸収体物質または製品は商業的分野に多様な用途を見 出すと思われる。今までは、これらの吸収体製品は通常、ウシドフラフまたはポ リマーゲルとウッドフラフとの組合せのような組成物から成る。これらの製品の 液体保留性(liquid retenttve property)は対象の 重要な特性をなし、「液体保留」なる用語は液体の量と保留の可逆性との両方を 含む、以下でさらに詳述するように、全吸収体の重量の2100%を越えるまで の量で液体を吸収し、保留する能力を有する浸透圧吸収体が製造されることが今 回発見された。Power station-9-Overview As previously mentioned, disposable absorbent materials or products find a variety of uses in the commercial field. I think it will be released. Until now, these absorbent products were typically made from bovine fluff or poultry. It consists of a composition such as a combination of Remargel and Wood Fluff. of these products Liquid retentve property is the target The term “liquid retention” refers to both the amount of liquid and the reversibility of the retention. up to more than 2100% of the total absorbent weight, as further detailed below. Osmotic absorbers can now be manufactured that have the ability to absorb and retain liquids in amounts of Found twice.
それ故、吸収体を提供することが本発明の目的である。It is therefore an object of the present invention to provide an absorbent body.
本発明の他の目的は、吸収体の重量を大きく越える量で液体を不可逆的に吸収す る能力を有する浸透圧吸収体を提供することである。Another object of the invention is to irreversibly absorb liquid in an amount significantly exceeding the weight of the absorbent body. The object of the present invention is to provide an osmotic absorber having the ability to
1形式では、本発明の実施態様は高オスモラリティ(os■olality)プ ロモーターを内部に含む、包被された(encapsulated)ポリマー半 透膜シェルから成る浸透圧吸収体にある。In one form, embodiments of the invention provide a high osmolality product. Encapsulated polymer half containing romator inside It is an osmotic pressure absorber consisting of a permeable membrane shell.
本発明の特定の実施態様は、包被されたセルロースアセテート製のポリマー半透 膜シェルから成り、前記膜シェルの厚さが約5〜約30ミクロンの範囲内であり 、その中に塩化ナトリウムから成る高オスモラリティプロモーターを含む浸透圧 吸収体にある。A particular embodiment of the invention is a polymeric semi-permeable material made of encapsulated cellulose acetate. comprising a membrane shell, the membrane shell having a thickness in the range of about 5 to about 30 microns; , which contains a high osmolality promoter consisting of sodium chloride. It's in the absorber.
見所q詳槻l説皿 前述したように、本発明は浸透圧吸収体に関する。これらの製品は内部に高オス モラリティプロモーターを含む、包被ポリマー半i3膜シェルから成る。これら の吸収体は多様の用途を見出す0例えば、高吸収値を有する物質は例えばベビー おむつのような使い捨て吸収体製品に用いられる。おむつは通常、約1%の濃度 を有する弱塩溶液である尿を吸収するように設計されている。現在、おむつ設計 は趙吸収体ポリマーと混合したウッドフラフを用いる。現在用いられている最も ボピエラーなポリマーは架橋ポリアクリル酸の誘導体であり、吸収体ゲル化剤( AGM)として一般に公知である。原溶液に関して、他の特定の設計制約(co −nstraint)を考慮して測定した場合に、AGMによる液体吸収が約3 0重量%に限定される。AGM膨潤の機構は主として浸透圧によるものであるが 、この機構は構造体内に包含される浸透圧プロモーターの重量%によって限定さ れる。これとは正反対に、本発明の浸透圧吸収体は任意に高められる濃度で浸透 圧プロモーターまたは高オスモラリティプロモーターを用いる。以下でさらに詳 述するように、種々なタイプの高オスモラリティプロモーターを用いることがで き、このことはAGMと浸透圧プロモーターとしてイオン種を併用することの限 度とは対照的である。それ故、本発明のプロモーターの高オスモラリティがこの ように制限されないという事実を考慮すると、本発明の浸透圧吸収体はAGMの 吸収容量を大きく凌駕する吸収容量を有することが発見されている。Highlights q Details Plate As mentioned above, the present invention relates to osmotic absorbers. These products have high male inside It consists of an encapsulated polymer semi-i3 membrane shell containing a morality promoter. these Absorbers find a wide variety of uses. For example, substances with high absorption values Used in disposable absorbent products such as diapers. Diapers usually have a concentration of about 1% It is designed to absorb urine, which is a weak salt solution with a Diaper design currently uses wood fluff mixed with a Zhao absorbent polymer. Most currently used The boppier polymer is a derivative of cross-linked polyacrylic acid and absorbent gelling agent ( AGM). Regarding the stock solution, certain other design constraints (co -nstraint), the liquid absorption by AGM is approximately 3 Limited to 0% by weight. The mechanism of AGM swelling is mainly due to osmotic pressure. , this mechanism is limited by the weight percent of the osmotic promoter contained within the construct. It will be done. In contrast, the osmotic absorbers of the present invention can be osmotic at arbitrarily elevated concentrations. Use pressure promoters or high osmolality promoters. More details below Various types of high osmolality promoters can be used, as described above. This is a limitation of the combined use of ionic species as AGM and osmotic promoters. In contrast to degree. Therefore, the high osmolarity of the promoter of the present invention is due to this Considering the fact that the osmotic absorber of the present invention is not limited to It has been discovered that it has an absorption capacity that greatly exceeds the absorption capacity.
上記考察はおむつ用途における浸透圧吸収体の使用に重点をおいたものであった が、前記吸収剤が使用する特定のポリマー膜シェルとオスモラリティプロモータ ーとに従って、他の方法で利用されることも本発明の範囲内で考えられる0例え ば、本発明の吸収体を用いて、例えば水のような好ましくない液体の存在が炭化 水素燃料の使用に不利な影響を及ぼす場合に、前記燃料から好ましくない液体を 除去することもできる。The above considerations focused on the use of osmotic pressure absorbers in diaper applications. However, the specific polymeric membrane shell and osmolarity promoter used by the absorbent It is within the scope of the present invention that it may also be utilized in other ways according to For example, using the absorbent body of the invention, the presence of undesirable liquids, such as water, can be prevented from carbonizing. Remove undesirable liquids from hydrogen fuels if they adversely affect the use of said fuels. It can also be removed.
本発明の浸透圧吸収は、既述したように、高オスモラリティプロモーターを内蔵 した包被ポリマー半透膜シェルから成る。VjL収体のシェル成分として用いら れるポリマー半透膜は浸透圧プロモーターを高度に拒絶すると共に良好な透水性 を有するポリマー膜である。これらの性質を有する膜は膜シェル中への良好な水 または液体の流入を可能にし、高い浸透圧差を形成する。ポリマー膜の幾つかの 代表的な例には、ジアセテートとトリアセテートを含めたセルロースアセテート 、例えばメチルセルロース、エチルセルロース、プロピルセルロース、ニトロセ ルロース等のようなセルロースアセテート誘導体、スルホン化ポリスルホン、例 えばポリスチレンスルホネートとポリベンジルトリメチルアンモニウムクロリド との複合体、例えばナイロン4、ナイロン6、ナイロン7、ナイロン8、ナイロ ン9、ナイロン66等のような種々なナイロンを含む長鎖ポリマーアミドから製 造されたもの、例えばポリエチレングリコールのようなポリエーテルと例えばト ルエンジイソシアネートのようなインシアネートとを反応させて、イソシアネー ト−キャップ付きポリエーテル(isocyanate−capped pol yether)を形成し、その後に前記ポリエーテルに例えばポリビニルピロリ ジンのような複素環式窒素含有化合物を混合することによって製造されるような 相互浸透性ポリマーネットワーク膜、例えばm−フェニレンジアミンのような芳 香族ポリアミンを例えばトリメソイルクロリドのような芳香族ポリカルボン酸ク ロリドと反応させて界面重合ポリマーを形成することによって製造される膜があ る。ポリマー自体をシェル自体として用いることができるが、ポリマーを例えば ポリスルホン、ポリカーボネート等のような多孔質サポートバッキング物質上に 支持することも、本発明の範囲内で考えられる。As mentioned above, the osmotic absorption of the present invention has a built-in high osmolality promoter. It consists of an encapsulated polymeric semipermeable membrane shell. Used as a shell component of VjL receptor Polymer semipermeable membrane highly rejects osmotic promoters and has good water permeability It is a polymer membrane with a Membranes with these properties have good water absorption into the membrane shell. or allow the influx of liquid and form a high osmotic pressure difference. Some of the polymer membranes Typical examples include cellulose acetate, including diacetate and triacetate. , such as methylcellulose, ethylcellulose, propylcellulose, nitrose Cellulose acetate derivatives such as lulose, sulfonated polysulfones, e.g. For example, polystyrene sulfonate and polybenzyltrimethylammonium chloride complexes with, such as nylon 4, nylon 6, nylon 7, nylon 8, nylon Made from long chain polymer amides including various nylons such as Nylon 9, Nylon 66, etc. manufactured products, such as polyethers such as polyethylene glycol and isocyanate by reacting with incyanate such as luene diisocyanate isocyanate-capped pol after which the polyether is coated with, for example, polyvinylpyrroli such as those produced by mixing heterocyclic nitrogen-containing compounds such as gin Interpenetrating polymer network membranes, e.g. For example, aromatic polyamines can be added to aromatic polycarboxylic acids such as trimesoyl chloride. There are membranes produced by reacting with loride to form interfacially polymerized polymers. Ru. Although the polymer itself can be used as the shell itself, e.g. on porous support backing materials like polysulfone, polycarbonate etc. Supporting is also contemplated within the scope of the invention.
吸収体の第2成分をなし、ポリマ・−膜シエル内に封入される高オスモラリティ プロモーターは膜による良好な拒絶率(rejection rate)を有す る低分子量水溶性成分であることが好ましい、これらの高オスモラリティプロモ ーターの幾つかの典型的な例には、例えば塩化リチウム、塩化ナトリウム、塩化 カリウム、塩化ルビジウム、塩化カルシウム、塩化バリウム、塩化マグネシウム 、シュウ化リチウム、シュウ化ナトリウム、シュウ化カリウム、シュウ化ルビジ ウム、シュウ化カルシウム、シェラ化バリウム、シュウ化マグネシウム等のよう な周期律表第■A族と第mA族のハリド塩;例えばグルコース、スクロース、フ ルクトース等のような糖;例えばグリセロール、エチレングリコールのような多 価アルコール化合物(polyhydric compound) ;例えば水 酸化アンモニウム、塩化アンモニウム等のようなアンモニウム化合物;乳酸;炭 酸水素カリウム、炭酸水素ナトリウム、炭酸水素ナトリウム等がある。膜層とし てのポリマーと浸透圧プロモーターとの上記リストが浸透圧吸収体の形成に用い ることのできる化合物の種類を代表するにすぎず、本発明が必ずしもこれに限定 されないことを理解すべきである。High osmolality, which forms the second component of the absorber and is encapsulated within a polymer membrane shell. The promoter has a good rejection rate by the membrane. These high osmolality promoters are preferably low molecular weight water-soluble components. Some typical examples of salts include, for example, lithium chloride, sodium chloride, Potassium, rubidium chloride, calcium chloride, barium chloride, magnesium chloride , lithium oxalide, sodium oxalide, potassium oxalide, rubidium oxalide such as calcium oxalide, barium oxalide, magnesium oxalide, etc. halide salts of groups A and mA of the periodic table; e.g. glucose, sucrose, Sugars such as luctose; polyesters such as glycerol, ethylene glycol, etc. Polyhydric compound; for example, water Ammonium compounds such as ammonium oxide, ammonium chloride etc; lactic acid; charcoal Potassium oxyhydrogen, sodium hydrogen carbonate, sodium hydrogen carbonate, etc. As a membrane layer The above list of polymers and osmotic promoters can be used to form osmotic absorbers. These are merely representative of the types of compounds that can be used, and the present invention is not necessarily limited thereto. It should be understood that this is not the case.
内部に浸透圧プロモーターを含む包被ポリマー半透膜シェルから成る浸透圧吸収 体は約2=1から約1=10までの範囲内のポリマー:プロモーターの重量比を 含む、好ましい液体吸収率を得るために、浸透圧プロモーターの使用量はポリマ ーの重量に依存する。後者の重量はこの場合ポリマー半透膜シェルの厚さに依存 し、本発明の好ましい実施態様では、前記厚さは約5〜約30ミクロンの範囲内 である。Osmotic absorption consisting of an encapsulated polymeric semipermeable membrane shell containing an osmotic promoter inside. The body has a polymer:promoter weight ratio in the range of about 2=1 to about 1=10. The amount of osmotic promoter used is determined by the amount of polymer - depends on the weight of the The weight of the latter depends in this case on the thickness of the polymer semipermeable membrane shell. However, in a preferred embodiment of the invention, the thickness is within the range of about 5 to about 30 microns. It is.
浸透圧吸収体の形状は非常に多様に変化しうる。浸透圧吸収体の形状の幾つかの 代表的な例にはシート、球、中空繊維等がある。これらの吸収体は技術上公知の 方法で製造される1例えば、浸透圧吸収体をシート形状にすべき場合は、浸透圧 プロモータ一層を膜の上層と下層との間に挿入し、次に前記層をラミネートして 、内部に封入された浸透圧プロモーターを含む包被シェルを形成する。同様に浸 透圧プロモーターは、特に固体形がある場合に、好ましいポリマーを塗布し、そ の後に処理して好ましい膜を形成する。同様に、浸透圧吸収体を中空繊維状にす べき場合には、この場合にも技術上公知の方法によって、繊維をポリマー半透膜 から形成し、その後に浸透圧プロモーターを繊維の長さの中に封入して、その後 にIIhm長さの各端部をシールして漏出を阻止する。The shape of the osmotic absorber can vary widely. Some shapes of osmotic absorbers Typical examples include sheets, spheres, hollow fibers, etc. These absorbers are known in the art. For example, if the osmotic pressure absorber is to be made into a sheet shape, the osmotic pressure Inserting one layer of promoter between the top and bottom layers of the membrane, then laminating said layers. , forming an enveloped shell containing an osmotic promoter encapsulated inside. Similarly, The tomopromoter, especially if there is a solid form, can be coated with a preferred polymer and its and subsequent processing to form the preferred film. Similarly, the osmotic pressure absorber can be made into hollow fibers. If necessary, the fibers are coated with a polymeric semipermeable membrane, again by methods known in the art. after which the osmotic promoter is encapsulated within the length of the fiber, and then Seal each end of the IIhm length to prevent leakage.
災−施一斑−1 この実施例では、3X3C1のサイズで、20ミクロンの厚さを有するポリマー のセルロースアセテートのシートを平坦な表面上に置いた。グルコースとスフロ スを含む、種々な量の浸透圧プロモーターをシートの中央に入れ、その後に第2 シートのポリマーセルロースアセテートを第1シートと浸透圧プロモーターとの 上部に置いた。ポリマーを軟化することによって縁部をシールし、各パケット( packe t)を秤量する。ポリマーセルロースアセテート内に封入されたオ スモラリティプロモーターから成る浸透圧吸収体パケットを水中に30分間〜3 60分間の範囲内の時間入れた。この後に、パケットを水から取り出し、吸収体 ペーパータオルで圧迫して乾燥させ、浸せき重量を得た。この試験の結果を下記 の第1表に示した0表中パケットA、B、C,Dは浸透圧プロモーターとして種 々な量のグルコースを含み、バケツ)Eは浸透圧プロモーターとしてスクロース を含んだ。Disaster - Disaster - 1 In this example, a polymer with a size of 3X3C1 and a thickness of 20 microns A sheet of cellulose acetate was placed on a flat surface. glucose and soufflo Varying amounts of osmotic promoters, including The polymer cellulose acetate of the sheet is combined with the first sheet and the osmotic pressure promoter. placed at the top. Seal the edges by softening the polymer and seal each packet ( Weigh the package t). O encapsulated in polymer cellulose acetate The osmotic absorber packet consisting of smolarity promoter is placed in water for 30 minutes. The time was set within 60 minutes. After this, remove the packet from the water and use the absorbent The soak weight was obtained by pressing dry with a paper towel. The results of this test are below Packets A, B, C, and D in Table 0 shown in Table 1 contain species as osmotic promoters. Buckets containing varying amounts of glucose) E is sucrose as an osmotic promoter. Contained.
第一1−表 0 0.043 LiC1;0.074 20m 7.0cm O0%30 2 128% 60 3170% 90 3979% P O,056LiC1;0.110 16111 11.5CIl O0%3 0 2404% 60 3212% Q O,070LiC1;0.112 22m 10.0c11 0 0%30 2313% 60 3416% 90 4180% 夫−族一斑−■ 上記実施例■に述べた方法と同し方法で、種々な量の塩化ナトリウムを上記例に 述べたちの同じ表面積と厚さとを有するセルロースアセテートから成るポリマー 半13WAシェル内に封入することによって、浸透圧吸収体パケットを製造した 。11-Table 0 0.043 LiC1; 0.074 20m 7.0cm O0%30 2 128% 60 3170% 90 3979% P O,056LiC1;0.110 16111 11.5CIl O0%3 0 2404% 60 3212% Q O,070LiC1;0.112 22m 10.0c11 0 0%30 2313% 60 3416% 90 4180% Husband - family member - ■ Various amounts of sodium chloride were added to the above example in the same manner as described in Example ■ above. A polymer consisting of cellulose acetate with the same surface area and thickness as mentioned. Osmotic absorber packets were manufactured by encapsulating within a semi-13WA shell. .
F、G、H1■およびJと名づけたパケットを水中に90分間〜1060分間の 範囲内の期間浸せきした。上記期間の終了時に、パケットを取出し、吸収体をペ ーパータオルで乾燥するまで軽くたたき、秤量した。これらの試験結果を下記の 第2表に示す。Packets named F, G, H1■ and J were placed in water for 90 to 1060 minutes. Soaked for a period within the range. At the end of the above period, remove the packet and insert the absorber. It was patted dry with a paper towel and weighed. These test results are shown below. Shown in Table 2.
箪−λ−表 F O,034NaC1;0.067 0.101 900.596 490% 1456%G O,050NaCl;0.036 0.0B6 3501.0 42 1112% 1912%HO,040NaCl;0.046 0.0B6 2400.875 917% 1973%1 0.251 NaCl;0.1 36 0.387 3006.221 1507% 2324%J O,187 NaC1;0.251 0.438 10609.616 2100% 490 8%実−施−flu 高オスモラリティプロモーターとして塩化ナトリウム、スクロースおよびグルコ ースを用い、ポリマー半透膜としてセルロースアセテートを用いて、上記例に述 べた方法と同じ方法で、4パケツトを製造したウパケットを製造し、シールした 後に、4パケツト中の3パケツトを水中に浸せきし、第4パケツトは1重量%塩 化ナトリウム含有溶液中に浸せきした。パケットを48時間までの期間浸せきし た。この48時間の期間中に、パケットを種々な間隔をおいて回収し、乾燥する まで軽くたたき、秤量した。これらの試験結果を下記の第3表と第4表に示す。箪-λ-table FO, 034NaCl; 0.067 0.101 900.596 490% 1456%G O, 050NaCl; 0.036 0.0B6 3501.0 42 1112% 1912% HO, 040NaCl; 0.046 0.0B6 2400.875 917% 1973%1 0.251 NaCl; 0.1 36 0.387 3006.221 1507% 2324% J O, 187 NaC1; 0.251 0.438 10609.616 2100% 490 8% implementation-flu Sodium chloride, sucrose and glucose as high osmolality promoters As described in the example above, using cellulose acetate as the polymeric semipermeable membrane. Using the same method as above, we manufactured 4 packets and sealed them. Later, 3 of the 4 packets were soaked in water, and the 4th packet was soaked with 1% salt by weight. immersed in a solution containing sodium chloride. Soak the packet for up to 48 hours Ta. During this 48 hour period, the packets are collected and dried at various intervals. and weighed. The results of these tests are shown in Tables 3 and 4 below.
試験では、パケットに、LおよびMを水中に浸せきし、パケットNは塩化ナトリ ウム溶液中に浸せきした。In the test, packets L and M were immersed in water, and packet N was immersed in sodium chloride. immersed in um solution.
第一1−表 ポリマー重量(6) 0.18? 0.056 0.212 0.158プロモ 一タ一本体 NaC1スクロール グルコース NaClプロモーター重量(8 ) 0.251 0.134 0.436 0.156第−土−l ボiマー とした KL M N ポリマー重量Cg) 0.187 0.056 0.212 0.158プロモ 一タ一本体 NaC1スクロール グルコース NaClプロモーター重量(8 ) 0.251 0.134 0.436 0.156−片間1分1 ’ o o o o 。11-Table Polymer weight (6) 0.18? 0.056 0.212 0.158 promo One body NaCl Scroll Glucose NaCl promoter weight (8 ) 0.251 0.134 0.436 0.156th-Sat-l I made it a bomber KL M N Polymer weight Cg) 0.187 0.056 0.212 0.158 Promo One body NaCl Scroll Glucose NaCl promoter weight (8 ) 0.251 0.134 0.436 0.156 - 1 minute 1' o o o o .
1.060 4908 − − − 上記表から、各パケットがプロモーター重量を基準として約2,000%以上の 吸収率を有し、ポリマー重量を基準にした吸水率は塩化ナトリウム溶液の2.1 62%から水4,600重量%を越えるまでの範囲内であった。@収率の比較は 、大きなオスモラリティを有する浸透圧プロモーターが小さいオスモラリティを 有する浸透圧プロモーターよりも大きな流れ(flux)を可能にすることを開 示する。さらに、1%塩化す) IJ ’Jム熔液を用いた試験での吸水量は溶 液中の塩化ナトリウムの存在がパケット内部と吸収溶液との間の塩勾配の差を抑 圧するかぎり低く、低い吸水率を生ずる。1.060 4908 − − − From the table above, it is clear that each packet contains approximately 2,000% or more of the promoter weight. The water absorption rate based on the weight of the polymer is 2.1 of that of sodium chloride solution. It ranged from 62% to over 4,600% water by weight. @Yield comparison , an osmotic promoter with a large osmolarity has a small osmolarity. It was discovered that the osmotic promoter allows for greater flux than the osmotic promoter. Show. In addition, the amount of water absorbed in the test using IJ'J molten liquid (1% chloride) was The presence of sodium chloride in the solution suppresses the difference in salt gradient between the inside of the packet and the absorption solution. As long as pressure is applied, low water absorption rate is produced.
実−施一斑−N 周囲が比較的大きい中空繊維をセルロースアセテートから製造した。繊維の長さ を選び、一端をシールし、種々な量の塩化リチウムを高オスモラリティプロモー ターとして中空繊維の内部に入れ、残りの端部をシールし、形成された浸透圧吸 収体をO,P、Qと名づけた。これらの長くて、薄いパケットを水中に90分間 まで浸せきし、定期的に取り出し、乾燥するまで軽くたたき、秤量した。これら の試験結果を下記第5表に記載する。Implementation - Implementation - N Hollow fibers with a relatively large circumference were made from cellulose acetate. fiber length , seal one end, and add various amounts of lithium chloride to the high osmolality promoter. The remaining ends are sealed and the osmotic suction formed is placed inside the hollow fiber as a The objects were named O, P, and Q. These long, thin packets are placed in water for 90 minutes. Soaked until dry, removed periodically, patted dry, and weighed. these The test results are listed in Table 5 below.
0 0.043 LiCl;0.074 20m 7.0cm O0%30 2 128% 60 3170% 90 3979% P O,056LiCl0.110 16111 11.5C1100%30 2404% 60 3212% Q 0.070 LiC1;0.112 22+m 10.0C1100%30 2313% 60 3416% 90 4180% 閑静頂査報告 1+n++au。、、、、、、、、、、−、、PCT/l;S 8910407 4国際調査報告 IJs B904074 S^ 314440 0.043 LiCl; 0.074 20m 7.0cm O0%30 2 128% 60 3170% 90 3979% P O,056LiCl0.110 16111 11.5C1100%30 2404% 60 3212% Q 0.070 LiC1; 0.112 22+m 10.0C1100%30 2313% 60 3416% 90 4180% Quiet summit inspection report 1+n++au. , , , , , , , -, , PCT/l;S 8910407 4 International search report IJs B904074 S^ 31444
Claims (11)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US24782888A | 1988-09-22 | 1988-09-22 | |
US247,828 | 1988-09-22 |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04500626A true JPH04500626A (en) | 1992-02-06 |
Family
ID=22936544
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1510167A Pending JPH04500626A (en) | 1988-09-22 | 1989-09-19 | osmotic absorbent |
Country Status (13)
Country | Link |
---|---|
EP (2) | EP0360565A1 (en) |
JP (1) | JPH04500626A (en) |
KR (1) | KR900701329A (en) |
CN (1) | CN1041707A (en) |
AU (1) | AU622936B2 (en) |
BR (1) | BR8907669A (en) |
DK (1) | DK48991A (en) |
FI (1) | FI911325A0 (en) |
MX (1) | MX170372B (en) |
MY (1) | MY104654A (en) |
NZ (1) | NZ230702A (en) |
PH (1) | PH26222A (en) |
WO (1) | WO1990003215A1 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5082723A (en) * | 1989-09-27 | 1992-01-21 | Kimberly-Clark Corporation | Osmotically enhanced absorbent structures |
US5108383A (en) * | 1989-12-08 | 1992-04-28 | Allied-Signal Inc. | Membranes for absorbent packets |
ATE170737T1 (en) | 1993-06-23 | 1998-09-15 | Procter & Gamble | DISPOSABLE ABSORBENT ARTICLE HAVING SELECTIVELY EXTENDABLE OR INFLATIVE COMPONENTS |
US5330459A (en) * | 1993-06-23 | 1994-07-19 | The Procter & Gamble Company | Disposable absorbent article having an inflatable spacer |
GB0714612D0 (en) * | 2007-07-26 | 2007-09-05 | Crilly Francis P | The antifungal surgical dressing |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3880164A (en) * | 1972-05-22 | 1975-04-29 | Alza Corp | Osmotic wound drain |
DE2964379D1 (en) * | 1978-11-25 | 1983-01-27 | Knut Stache | Apparatus for producing a potable liquid from sea-water, polluted water and the like by osmosis |
SE431934B (en) * | 1981-12-11 | 1984-03-12 | Carl Gustaf Kamme | ABSORPTION BODY WITH SEMIPERMEABLE MEMBRANE |
JPS61249341A (en) * | 1985-04-27 | 1986-11-06 | Showa Denko Kk | Dehydrating tool |
JPS62272934A (en) * | 1986-05-21 | 1987-11-27 | Showa Denko Kk | Method for treating tuna |
JPH0740913B2 (en) * | 1986-10-29 | 1995-05-10 | 株式会社リブ・インタ−ナシヨナル | How to adjust the quality of liquor |
-
1989
- 1989-09-15 MY MYPI89001260A patent/MY104654A/en unknown
- 1989-09-19 JP JP1510167A patent/JPH04500626A/en active Pending
- 1989-09-19 EP EP89309528A patent/EP0360565A1/en not_active Withdrawn
- 1989-09-19 KR KR1019900700893A patent/KR900701329A/en not_active Application Discontinuation
- 1989-09-19 AU AU43258/89A patent/AU622936B2/en not_active Ceased
- 1989-09-19 NZ NZ230702A patent/NZ230702A/en unknown
- 1989-09-19 BR BR898907669A patent/BR8907669A/en not_active Application Discontinuation
- 1989-09-19 EP EP19890910969 patent/EP0435931A1/en active Pending
- 1989-09-19 WO PCT/US1989/004074 patent/WO1990003215A1/en not_active Application Discontinuation
- 1989-09-20 PH PH39255A patent/PH26222A/en unknown
- 1989-09-21 CN CN89107444A patent/CN1041707A/en active Pending
- 1989-10-04 MX MX017817A patent/MX170372B/en unknown
-
1991
- 1991-03-19 FI FI911325A patent/FI911325A0/en not_active Application Discontinuation
- 1991-03-19 DK DK048991A patent/DK48991A/en unknown
Also Published As
Publication number | Publication date |
---|---|
EP0360565A1 (en) | 1990-03-28 |
FI911325A0 (en) | 1991-03-19 |
AU622936B2 (en) | 1992-04-30 |
BR8907669A (en) | 1991-07-30 |
DK48991D0 (en) | 1991-03-19 |
AU4325889A (en) | 1990-04-18 |
MY104654A (en) | 1994-05-31 |
WO1990003215A1 (en) | 1990-04-05 |
EP0435931A1 (en) | 1991-07-10 |
KR900701329A (en) | 1990-12-01 |
PH26222A (en) | 1992-04-01 |
CN1041707A (en) | 1990-05-02 |
NZ230702A (en) | 1991-10-25 |
MX170372B (en) | 1993-08-18 |
DK48991A (en) | 1991-05-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU631475B2 (en) | Membranes for absorbent packets | |
KR100432463B1 (en) | Polysulfone Hollow Fiber Membrane | |
US4720343A (en) | Macroporous asymmetrical hydrophilic membrane made of a synthetic polymer | |
US3371666A (en) | Absorbent device | |
KR0153471B1 (en) | Osmotically enhanced absorbent structure | |
KR100715867B1 (en) | Method for manufacture of films containing insoluble solids embedded in cellulose-based films | |
US4075108A (en) | Polycarbonate membranes and production thereof | |
EP0547474A1 (en) | Method for immobilizing superabsorbent polymer and products derived therefrom | |
US4160791A (en) | Polycarbonate membranes and production thereof | |
JPH01107812A (en) | Method for making porous membrane hydrophilic | |
JPH03278835A (en) | Heat radiating substance-adsorbing material | |
JPH04500626A (en) | osmotic absorbent | |
SE517075C2 (en) | Polysaccharide-based absorbent polymer material | |
TWI227703B (en) | Method to absorb dyestuff by crosslinked chitosan beads | |
CA1107467A (en) | Polycarbonate membranes for use in hemodialysis | |
Paul et al. | Acetylsalicylic acid loaded poly (vinyl alcohol) hemodialysis membranes: effect of drug release on blood compatibility and permeability | |
JPH03174231A (en) | Polyether ketone semi- permeable membrane | |
Ma et al. | Preparation and characterization of novel sodium alginate/chitosan two ply composite membranes | |
JP4110806B2 (en) | Toxic adsorbent for extracorporeal circulation | |
JP3327983B2 (en) | Dehumidifier composition | |
US4308145A (en) | Relatively thick polycarbonate membranes for use in hemodialysis | |
Chandy et al. | Preparation and performance of chitosan encapsulated activated charcoal (ACCB) adsorbents for small molecules | |
Mishra et al. | Preparation and characterization of polyvinyl alcohol based biomaterials: water sorption and in vitro blood compatibility study | |
NO135162B (en) | ||
JPH0424087B2 (en) |